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Modern Engineering Thermodynamics

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11.10 Compressibility Factor and Generalized Charts 385<br />

dimensionless equation of state. He defined the<br />

dimensionless variables reduced pressure p R , reduced<br />

temperature T R ,andreduced specific volume v r as 4<br />

p R = p/p c<br />

(11.38a)<br />

van der Waals<br />

isotherms<br />

T R = T/T c<br />

v R = v/v c<br />

(11.38b)<br />

(11.38c)<br />

where p and T are the actual pressure and temperature of<br />

the gas, and p c and T c are the critical state pressure and<br />

temperature of the gas (see Table C.12 in Thermodynamic<br />

Tables to accompany <strong>Modern</strong> <strong>Engineering</strong> <strong>Thermodynamics</strong>).<br />

Then, he hypothesized that p R = p R (v R , T R ) would define<br />

a generalized dimensionless equation of state that<br />

would be valid for all substances. Today, this hypothesis<br />

is called van der Waals’s law of corresponding states, but<br />

unfortunately, it has been found to be valid only for<br />

materials with similar molecular structures.<br />

In 1883, van der Waals introduced his now classical equation of state:<br />

p = RT/ðv − bÞ − a/v 2 (3.44)<br />

in which the constants a and b are corrections for intermolecular forces and molecular volume, respectively. This<br />

is a cubic equation in v (see Example 11.11) and has isotherms shaped as shown in Figure 11.3. For given<br />

p and T < T c values, there are three real roots of this equation. One root corresponds to v f , another corresponds<br />

to v g , and the third is a meaningless root between v f and v g .<br />

Van der Waals noted that the critical temperature isotherm seemed to have an inflection point at the critical<br />

point. If this were generally true, then all equations of state would have to obey the mathematical constraints of<br />

an inflection point, or<br />

<br />

∂p<br />

=<br />

∂v<br />

Tc,v ∂2 p<br />

c ∂v<br />

Tc,v 2 = 0<br />

c<br />

Applying these conditions to the van der Waals equation yields<br />

and<br />

<br />

∂p Tc<br />

= RT c / ðv c − bÞ 2 + 2a/vc 3 ∂v<br />

= 0<br />

,v c<br />

<br />

∂ 2 <br />

p Tc<br />

∂v 2 = 2RT c / ðv c − bÞ 3 − 6a/vc 4 = 0<br />

,v c<br />

and solving these two equations simultaneously for a and b while using Eq. (3.44) evaluated at the critical point<br />

gives<br />

and<br />

a = 9RT c v c /8 = 27<br />

<br />

R 2 Tc<br />

2 <br />

64 p c<br />

b = v c /3 = RT c<br />

8p c<br />

Specific volume, v<br />

Thus, if the van der Waals equation accurately represented universal material behavior, the constants a and b<br />

could be determined from a single experimental measurement at the critical point.<br />

Pressure, p<br />

Vapor dome<br />

Actual<br />

isotherm<br />

FIGURE 11.3<br />

Schematic of van der Waals isotherms near the vapor dome.<br />

4 Note that the reduced properties p R and v R are not the same as the relative properties p r and v r introduced in the previous section.

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